Separation of Cobalt and Nickel Ions Using Electrodialysis Reversal in the Presence of Ethylene Diamine Tetraacetic Acid

Hiroshi Takahashi, Kasumi Takahashi, K. Fujita, T. Nishide
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Abstract

This paper describes selective separation of cobalt and nickel ions from their mixed solution using the electrodialysis reversal (ED-R) process. In experiments using the conventional electrodialysis process, the fluxes of cobalt and nickel ions were almost identical under the conditions used. Conversely, when electrodialysis experiments were conducted in the presence of Ethylene Diamine Tetraacetic Acid (EDTA), cobalt ions preferentially permeated through a cation-exchange membrane and were well separated. Based on these results, cobalt and nickel ions were permeated into a compartment containing an EDTA aqueous solution by normal electrodialysis operation, and then ED-R was performed with the polarity reversed to separate the cobalt and nickel ions. The ED-R -operation facilitated to effectively separate the nickel and cobalt ions. We also attempted to recover the nickel ions and EDTA from their mixed solution using a precipitation method. The recovery rate of EDTA reached 80 % , and the solution turned green at a lower pH of 0.4.
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乙二胺四乙酸存在下电渗析反转分离钴镍离子
本文介绍了利用电渗析反转(ED-R)工艺从混合溶液中选择性分离钴和镍离子。在使用传统电渗析工艺的实验中,在使用的条件下,钴离子和镍离子的通量几乎相同。相反,当电渗析实验在乙二胺四乙酸(EDTA)存在下进行时,钴离子优先通过阳离子交换膜渗透并被很好地分离。在此基础上,通过常规电渗析操作将钴和镍离子渗透到含有EDTA水溶液的隔室中,然后进行极性反转的ED-R以分离钴和镍离子。ED-R操作有利于镍钴离子的有效分离。我们还尝试用沉淀法从它们的混合溶液中回收镍离子和EDTA。EDTA的回收率达到80%,在较低的pH为0.4时,溶液呈现绿色。
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